US4783501A - Method for preparing a polymeric composition - Google Patents
Method for preparing a polymeric composition Download PDFInfo
- Publication number
- US4783501A US4783501A US06/898,496 US89849686A US4783501A US 4783501 A US4783501 A US 4783501A US 89849686 A US89849686 A US 89849686A US 4783501 A US4783501 A US 4783501A
- Authority
- US
- United States
- Prior art keywords
- monomer
- inorganic compound
- sup
- parts
- radical
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08F—MACROMOLECULAR COMPOUNDS OBTAINED BY REACTIONS ONLY INVOLVING CARBON-TO-CARBON UNSATURATED BONDS
- C08F292/00—Macromolecular compounds obtained by polymerising monomers on to inorganic materials
Definitions
- the present invention relates to a novel method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer.
- the present inventors have previously proposed a method for firmly consolidating an inorganic compound and an organic polymer, wherein a radical polymerizable vinyl monomer and an inorganic compound as a third component are contacted in the presence of a certain specific organic acid monomer or organic acid salt monomer (U.S. Pat. No. 4,435,540, issued on Mar. 6, 1984).
- this method is based on the non-catalytic polymerization of the vinyl monomer by the contact of the specific organic acid monomer or organic acid salt monomer with the inorganic compound, and thus has a problem that the degree of polymerization of the monomer and the graft rate i.e.
- the ratio of the organic polymer firmly consolidated to the formed polymer are not necessarily adequate.
- the applicable vinyl monomer is restricted to the one composed mainly of methyl acrylate or methyl methacrylate, and thus has a drawback that the useful monomer is rather limited.
- the present invention provides a method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer, which comprises polymerizing at least one radical polymerizable vinyl monomer in an aqueous medium polymerization system comprising an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, by using a radical polymerization initiator.
- the organic acid monomer or organic acid salt monomer is preferably a sulfonic acid monomer or sulfonate monomer of the formula: ##STR1## wherein R 1 is a hydrogen atom, a C 1 -C 20 alkyl group or a halogen atom, X is ##STR2## (wherein each of R 2 and R 3 is a hydrogen atom or a C 1 -C 15 alkyl group, and R 4 is a C 1 -C 15 alkylene group), -COO(CH 2 m (wherein m is an integer of 1 to 20) or CH 2 n (wherein n is an integer of 0 to 20), and Y is a hydrogen atom, an ammonium radical or an alkali metal atom; or a carboxylic acid monomer or carboxylate monomer of the formula: ##STR3## wherein each of R 5 and R 6 is a hydrogen atom, a C 1 -C 15 alkyl group or --COOA (wherein A
- a feature of the present invention is that the interaction between the surface of the inorganic compound and the polymer formed according to the method of the present invention, is derived from a firmly consolidated chemical bond beyond simple adsorption or physical adhesion by e.g. van der Waals adsorption.
- an inorganic compound is suspended and dispersed in an aqueous medium at a temperature within a range in which a radical polymerization initiator decomposes, and an organic vinyl monomer, a specific organic acid monomer or organic acid salt monomer and a radical polymerization initiator are added and stirred to conduct aqueous heterogeneous polymerization, whereupon a copolymer of the vinyl monomer with the organic acid monomer or organic acid salt monomer is uniformly and firmly bonded to the surface of the inorganic compound with a high degree of polymerization and graft rate in a predetermined period of polymerization.
- the sulfonic acid monomer or sulfonate monomer of the formula I is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a sulfonic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the inorganic compound and the resulting polymer. Any compound having a structure containing these functional groups can be employed.
- AMS 2-acrylamido-2-methylpropanesulfonic acid
- SEM-Na sodium 2-methacryloylethanesulfonate
- SPS sodium 3-methacryloylpropanesulfonate
- NaAS sodium 2-propenesulfonate
- NaMS sodium 2-methyl-2-propenesulfonate
- the carboxylic acid monomer or carboxylate monomer of the formulas II and III is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a carboxylic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the organic compound and the formed polymer.
- Any compound having a structure containing these functional groups may be employed.
- acrylic acid, methacrylic acid, crotonic acid, tiglic acid, cinnamic acid, maleic anhydride and citraconic anhydride particularly preferred are acrylic acid, methacrylic acid, crotonic acid and maleic anhydride, as they have high polymerization activities and graft efficiency (i.e. efficiency for firm consolidation of the formed polymer).
- a carbide, nitride or boride of silicon or zirconium, or zirconium oxide is particularly preferred, in view of remarkable effects for the activation of the vinyl monomer and for the firm consolidation with the polymer.
- any conventional radical polymerizable vinyl monomer may be employed.
- radical polymerization initiator to be used in the present invention any conventional peroxide or azo compound may be employed.
- a radical polymerization initiator which is decomposable at a temperature within a range of from 40°to 100° C. is particularly useful.
- peroxides such as benzoyl peroxide, azobisisobutyronitrile and potassium persulfate, and azo compounds.
- the polymeric composition after the reaction was thoroughly dried at 105° C. for one day and night, and then about 5 g of the composition was completely burned at 650° C. for 3 hours, whereupon the amount of the polymer consolidated to the inorganic compound was calculated from the weight reduction. Then, the consolidation rate was obtained in accordance with the following formula: ##EQU1##
- Example 1 and Comparative Examples 1 to 3 as shown in Table 1 were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylforamide, as good solvents for methyl methacrylate-SEM-Na copolymers, whereby the reduction in the polymer contents was studied.
- the results are shown in Table 2.
- the polymer content after being thoroughly extracted with dimethylformamide for 200 hours was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond.
- compositions Comparative Examples 4 and 5 wherein an inorganic powder (silicon nitride) was coated with a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-SEM-Na copolymer whereby the reduction in the polymer content was compared.
- Example 1 in Example 1 according to the method of the present invention wherein a radical polymerization initiator was added in the presence of a sulfonic acid monomer or sulfonate monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.
- the graft efficiency is higher with lipophilic radical polymerization initiators such as BPO, LPO and AIBN than with water-soluble AIBA and KPS.
- Example 6 The reaction was conducted in the same manner as in Example 1 except that the type of the inorganic compound was changed, and the composition thereby obtained was evaluated. The results are shown in Table 6.
- the method of the present invention is superior to the conventional noncatalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.
- Example 14 and Comparative Examples 10 to 12 as shown in Table 8 were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide, as good solvents for methyl methacrylate-methacrylic acid copolymers, whereby the reduction in the polymer contents was studied.
- the results are shown in Table 9.
- the polymer content after being thoroughly extracted with dimethylformamide for 200 hours was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond.
- compositions Comparative Examples 13 and 14
- an inorganic powder silicon nitride
- a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-methacrylic acid copolymer whereby the reduction in the polymer content was compared.
- Example 14 wherein a radical polymerization initiator was added in the presence of a carboxylic acid monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.
- the polymerization was carried out in the same manner as in Example 14, except that acrylic acid, crotonic acid, tiglic acid, cinnamic acid or maleic anhydride was used as the carboxylic acid monomer instead of methacrylic acid.
- the graft efficiency was measured, and the results are shown in Table 10.
- the method of the present invention is superior to the conventional noncatalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.
Abstract
A method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer, which comprises polymerizing at least one radical polymerizable vinyl monomer in an aqueous medium polymerization system comprising an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, by using a radical polymerization initiator.
Description
The present invention relates to a novel method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer.
Heretofore, there have been active researches for the development of composite materials, wherein two or more materials are combined to mutually complement the properties of the respective materials to present a new useful function. In recent years, an attention has been drawn not only to mere application of an inorganic compound powder to a composite material as a filler, but also to a composite material such as a ceramic material, a magnetic material or a dental material, wherein a powder of an inorganic compound having a high level of function imparted thereto is combined with an organic polymer. However, in this case, the materials to be combined are mutually substantially different in their properties, and the interfacial affinity such as the compatibility or adhesion is poor. Thus, such a combination has inherent drawbacks such that the effectiveness of the combination can not adequately be improved, and the function of the inorganic compound powder itself can hardly adequately be utilized.
Various methods for modifying the surface properties of a powder have been proposed to overcome these drawbacks, to improve the interfacial affinity of the inorganic compound with the organic polymer substance and to attain high packing density, uniform dispersion and high strength. For instance, there may be mentioned a mechano-chemical method in which an inorganic compound is pulverized in the presence of a reactive monomer, followed by grafting an organic polymer, or a radiation method wherein an inorganic substance is irradiated with a high-energy radiation to be grafted with an organic polymer. These methods, however, require a grinding step or installation of a radiation equipment, resulting in complication of the manufacturing process and increase of the manufacturing cost, and present difficult problems for the practicability of the process.
Further, as an example for the surface modification of a powder in which an in situ polymerization for microcapsulation is employed, the present inventors have previously proposed a method for firmly consolidating an inorganic compound and an organic polymer, wherein a radical polymerizable vinyl monomer and an inorganic compound as a third component are contacted in the presence of a certain specific organic acid monomer or organic acid salt monomer (U.S. Pat. No. 4,435,540, issued on Mar. 6, 1984). However, this method is based on the non-catalytic polymerization of the vinyl monomer by the contact of the specific organic acid monomer or organic acid salt monomer with the inorganic compound, and thus has a problem that the degree of polymerization of the monomer and the graft rate i.e. the ratio of the organic polymer firmly consolidated to the formed polymer, are not necessarily adequate. Further, the applicable vinyl monomer is restricted to the one composed mainly of methyl acrylate or methyl methacrylate, and thus has a drawback that the useful monomer is rather limited.
It is an object of the present invention to provide a polymeric composition in which an organic polymer is uniformly and firmly bonded to the surface of an inorganic compound with a remarkably high degree of polymerization and graft rate.
The present invention provides a method for preparing a polymeric composition in which an inorganic compound is firmly consolidated in an organic polymer, which comprises polymerizing at least one radical polymerizable vinyl monomer in an aqueous medium polymerization system comprising an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, by using a radical polymerization initiator.
Now, the present invention will be described in detail with reference to the preferred embodiments.
The organic acid monomer or organic acid salt monomer is preferably a sulfonic acid monomer or sulfonate monomer of the formula: ##STR1## wherein R1 is a hydrogen atom, a C1 -C20 alkyl group or a halogen atom, X is ##STR2## (wherein each of R2 and R3 is a hydrogen atom or a C1 -C15 alkyl group, and R4 is a C1 -C15 alkylene group), -COO(CH2 m (wherein m is an integer of 1 to 20) or CH2 n (wherein n is an integer of 0 to 20), and Y is a hydrogen atom, an ammonium radical or an alkali metal atom; or a carboxylic acid monomer or carboxylate monomer of the formula: ##STR3## wherein each of R5 and R6 is a hydrogen atom, a C1 -C15 alkyl group or --COOA (wherein A is a hydrogen atom, an ammonium radical or an alkali metal atom), R7 is a hydrogen atom or a C1 -C15 alkyl group, Z is a hydrogen atom, an ammonium radical or an alkali metal atom, and each of R8 and R9 is a hydrogen atom or a C1 -C15 alkyl group.
A feature of the present invention is that the interaction between the surface of the inorganic compound and the polymer formed according to the method of the present invention, is derived from a firmly consolidated chemical bond beyond simple adsorption or physical adhesion by e.g. van der Waals adsorption.
Referring to a specific manner for carrying out the present invention, an inorganic compound is suspended and dispersed in an aqueous medium at a temperature within a range in which a radical polymerization initiator decomposes, and an organic vinyl monomer, a specific organic acid monomer or organic acid salt monomer and a radical polymerization initiator are added and stirred to conduct aqueous heterogeneous polymerization, whereupon a copolymer of the vinyl monomer with the organic acid monomer or organic acid salt monomer is uniformly and firmly bonded to the surface of the inorganic compound with a high degree of polymerization and graft rate in a predetermined period of polymerization.
In this case, if a usual dispersant such as a polyanion is used, the effect of the present invention can not be obtained.
The sulfonic acid monomer or sulfonate monomer of the formula I is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a sulfonic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the inorganic compound and the resulting polymer. Any compound having a structure containing these functional groups can be employed. For instance, there may be employed 2-acrylamido-2-methylpropanesulfonic acid (hereinafter referred to simply as AMS), sodium 2-methacryloylethanesulfonate (hereinafter referred to simply as SEM-Na), sodium 3-methacryloylpropanesulfonate (hereinafter referred to simply as SPS), sodium 2-propenesulfonate (hereinafter referred to simply as NaAS) and sodium 2-methyl-2-propenesulfonate (hereinafter referred to simply as NaMS). Among them, particularly preferred are AMS containing an amide linkage and SEM-Na and SPS containing an ester linkage, as they have high polymerization activities and graft efficiency (i.e. efficiency for firm consolidation of the formed polymer).
The carboxylic acid monomer or carboxylate monomer of the formulas II and III, is required to have a double bond as an active site attributable to the polymerizability by a radical polymerization initiator and a carboxylic acid group as an active site which brings about a firm consolidation by the interaction with hydroxyl groups present on the surface of the organic compound and the formed polymer. Any compound having a structure containing these functional groups may be employed. For instance, there may be mentioned acrylic acid, methacrylic acid, crotonic acid, tiglic acid, cinnamic acid, maleic anhydride and citraconic anhydride. Among them, particularly preferred are acrylic acid, methacrylic acid, crotonic acid and maleic anhydride, as they have high polymerization activities and graft efficiency (i.e. efficiency for firm consolidation of the formed polymer).
As the inorganic compound to be used in the present invention, a carbide, nitride or boride of silicon or zirconium, or zirconium oxide is particularly preferred, in view of remarkable effects for the activation of the vinyl monomer and for the firm consolidation with the polymer.
As the vinyl monomer to be used in the present invention, any conventional radical polymerizable vinyl monomer may be employed.
As the radical polymerization initiator to be used in the present invention, any conventional peroxide or azo compound may be employed. However, a radical polymerization initiator which is decomposable at a temperature within a range of from 40°to 100° C. is particularly useful. Among them, particularly preferred from the viewpoint of the graft rate are peroxides such as benzoyl peroxide, azobisisobutyronitrile and potassium persulfate, and azo compounds.
Now, the present invention will be described in further detail with reference to Examples. However, it should be understood that the present invention is by no means restricted by these specific Examples. In the Examples and Comparative Examples, the term "parts" means "parts by weight" unless otherwise specified.
EXAMPLE 1 and COMPARATIVE EXAMPLES 1 to 5
In a 1000 ml four-necked flask equipped with a condensor, a nitrogen inlet, a stirrer and a thermocouple for detecting the internal temperature, 270.0 g of silicon nitride, used as the inorganic compound, was suspended in 700 ml of deionized water to form a dispersion. After flushing the flask with nitrogen for 30 minutes, 28.0 g of methyl methacrylate, used as the vinyl monomer, was added to the dispersion with vigorous stirring under a nitrogen stream. Then, the above reaction mixture was heated to 70° C. in a warm water bath. After confirming the uniform dispersion of the added monomer, a solution of 10.0 g of SEM-Na as the sulfonate monomer in 20 ml of deionized water and a solution of 1.0 g of benzoyl peroxide as the radical initiator in 2.0 g of methyl methacrylate, were gradually added thereto. The mixture was reacted for polymerization at the same temperature for 8 hours. After completion of the polymerization, about 5 g of the reaction mixture was sampled. The sample was tested for the amount of the remaining unreacted monomer by gas chromatography using dioxane as internal standard, and the conversion was obtained.
Further, the polymeric composition after the reaction was thoroughly dried at 105° C. for one day and night, and then about 5 g of the composition was completely burned at 650° C. for 3 hours, whereupon the amount of the polymer consolidated to the inorganic compound was calculated from the weight reduction. Then, the consolidation rate was obtained in accordance with the following formula: ##EQU1##
For the purpose of comparison, similar polymerization operation and evaluation after the polymerization were conducted with respect to the polymerization behavior in the cases where the radical initiator was omitted as in the conventional non-catalytic polymerization system, the sulfonic acid monomer or sulfonate monomer was not added, and a dispersant was added. The results are shown in Table 1.
TABLE 1
__________________________________________________________________________
Sulfonate
Radical Vinyl Inorganic
monomer
polymerization
monomer
compound
Dispersant
Deionized
Conversion
Consolida-
SEM-Na
initiator
MMA Silicon nitride
Sodium hexa-
water of monomer
tion rate
(parts)*.sup.1
BPO (parts)
(parts)
(parts)*.sup.2
metaphosphate
(parts)
(%) (%)*.sup.3
__________________________________________________________________________
Example 1
10.0 1.0 30.0 270.0 -- 720 -100 96
Comparative
10.0 -- 30.0 270.0 -- 720 71 88
Example 1
Comparative
-- 1.0 30.0 270.0 -- 720 90 4
Example 2
Comparative
10.0 1.0 30.0 270.0 3.0 720 95 45
Example 3
__________________________________________________________________________
*.sup.1 CH.sub.2C.CH.sub.3COOC.sub.2 H.sub.4SO.sub.3 Na
*.sup.2 Special grade reagent
##STR4##
BPO: Benzoyl peroxide, MMA: Methyl methacrylate
It is evident from Table 1 that in the system of Comparative Example 2 wherein no sulfonic acid monomer or sulfonate monomer was added, the consolidation rate was very poor although a high conversion was obtainable, and a tendency for the separation of the inorganic compound and the homopolymer was observed. Further, it is evident that as compared with Comparative Example 1, the method of the present invention (Example 1) wherein a radical polymerization initiator was added, is superior in both the conversion of monomer and the consolidation rate. Further, in the system of Comparative Example 3 wherein a dispersant was added, the consolidation rate was substantially low, and a tendency for the separation of the homopolymer was observed as in the case of Comparative Example 2.
The polymeric compositions of Example 1 and Comparative Examples 1 to 3 as shown in Table 1, were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylforamide, as good solvents for methyl methacrylate-SEM-Na copolymers, whereby the reduction in the polymer contents was studied. The results are shown in Table 2. Here, the polymer content after being thoroughly extracted with dimethylformamide for 200 hours, was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond. For the purpose of comparison, a similar extraction operation was conducted with respect to each of compositions (Comparative Examples 4 and 5) wherein an inorganic powder (silicon nitride) was coated with a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-SEM-Na copolymer whereby the reduction in the polymer content was compared.
TABLE 2
__________________________________________________________________________
Polymer content
Graft
Preparation of Polymer content before
continuous extraction*.sup.4
efficiency*.sup.5
6
polymeric composition*.sup.1
extraction (%)
(graft rate)
(%)
__________________________________________________________________________
Polymerization system
Example 1 Presence of SEM-Na (Present invention)
9.6 9.1 90
Comparative Example 1
Non-catalytic polymerization system
6.5 1.8 23
without addition of BPO
Comparative Example 2
No addition of SEM-Na as opposed
1.1 -0.0 -0
to Example 1
Comparative Example 3
Addition of dispersant as opposed
4.5 0.9 8.6
to Example 1
Blend system
Comparative Example 4
Solvent blend of polymethyl
9.6 -0.0 --
methacrylate*.sup.2
Comparative Example 5
Solvent blend of methyl methacrylate-
9.5 -0.0 --
SEM-Na copolymer*.sup.3
__________________________________________________________________________
*.sup.1 Silicon nitride was used as the inorganic compound.
*.sup.2 Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd., was
used.
*.sup.3 A copolymer prepared in the same manner as in Example 1 except
that the method of the present invention was conducted in the absence of
the inorganic compound, was used.
*.sup.4 Continuous extraction by Soxhlet for 50 hours with benzene, 50
hours with acetone and 200 hours with dimethylformamide.
##STR5##
The polymer components in the compositions of Comparative Examples 2, 4 an 5 were completely extracted by the above continuous extraction operation irrespective of the system being of a polymerization type or of a solvent blend type. This indicates that even in the polymerization system, a polymer forming in the absence of a sulfonic acid monomer or sulfonate monomer, is merely chemically or physically adsorbed on the surface of the inorganic compound. In Comparative Examples 1 and 3, a part of the formed polymer was firmly consolidated to the inorganic compound, but the level of the graft rate was very low. Whereas, in Example 1 according to the method of the present invention wherein a radical polymerization initiator was added in the presence of a sulfonic acid monomer or sulfonate monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.
The polymerization was carried out in the same manner as in Example 1, except that SPS, AMS, NaAS or NaMS was used as the sulfonic acid monomer or sulfonate monomer instead of SEM-Na. The graft efficiency was measured, and the results are shown in Table 3.
TABLE 3
__________________________________________________________________________
Inorganic Graft
Radical polymeri-
Vinyl compound
Deionized
effi-
Acid Amounts
zation initiator
monomer
Silicon water ciency
monomer (parts)
BPO (parts)
MMA (parts)
nitride(parts)
(parts)
(%)
__________________________________________________________________________
Example 1
SEM-Na
10.0 1.0 30.0 270.0 720 90
Example 2
SPS*.sup.1
10.5 1.0 30.0 270.0 720 92
Example 3
AMS*.sup.2
9.9 1.0 30.0 270.0 720 90
Example 4
NaAS*.sup.3
6.5 1.0 30.0 270.0 720 75
Example 5
NaMS*.sup.4
7.1 1.0 30.0 270.0 720 78
__________________________________________________________________________
*.sup.1 CH.sub.2 ═C.CH.sub.3 --COOC.sub.3 H.sub.6 --SO.sub.3 Na
*.sup.2 CH.sub.2 ═CH--CONH--(CCH.sub.3).sub.2 CH.sub.2 SO.sub.3 H
*.sup.3 CH.sub.2 ═CHCH.sub.2 SO.sub.3 Na
*.sup.4 CH.sub.2 ═C.CH.sub.3 --CH.sub.2 SO.sub.3 Na
As is apparent from Table 3, the graft efficiency was very high with SEM-Na, SPS and AMS.
The reaction was conducted in the same manner as in Example 1 except that the type of the radical polymerization initiator was changed, and the compositions thereby obtained were evaluated. The results are shown in Table 4.
TABLE 4
__________________________________________________________________________
Acid Inorganic Graft
Radical monomer
Vinyl compound
Deionized
effi-
polymeriza- Amount
SEM-Na
monomer
Silicon
water ciency
tion initiator
(parts)
(parts)
MMA (parts)
nitride(parts)
(parts)
(%)
__________________________________________________________________________
Example 1
BPO 1.0 10.0 30.0 270.0 720 90
Example 6
LPO*.sup.1
1.0 10.0 30.0 270.0 720 93
Example 7
AIBN*.sup.2
1.0 10.0 30.0 270.0 720 90
Example 8
AIBA*.sup.3
1.0 10.0 30.0 270.0 720 70
Example 9
KPS*.sup.4
1.0 10.0 30.0 270.0 720 73
__________________________________________________________________________
*.sup.1 Lauroyl peroxide
*.sup.2 Azobisisobutyronitrile
*.sup.3 2,2'-Azobis(2-aminodipropane)hydrochloride
*.sup.4 Potassium persulfate
As is apparent from Table 4, the graft efficiency is higher with lipophilic radical polymerization initiators such as BPO, LPO and AIBN than with water-soluble AIBA and KPS.
The reaction was conducted in the same manner as in Example 1 except that the vinyl monomer identified in Table 5 was used instead of methyl methacrylate as the vinyl monomer, and the compositions thereby obtained were evaluated. The results are shown in Table 5.
TABLE 5
__________________________________________________________________________
Acid Inorganic Graft
monomer
Radical polymeri-
compound
Deionized
effi-
Vinyl Amount
SEM-Na
zation Silicon
water ciency
monomer (parts)
(parts)
BPO (parts)
nitride(parts)
(parts)
(%)
__________________________________________________________________________
Example 1
MMA 30.0 10.0 1.0 270.0 720 90
Example 10
ST 30.0 10.0 1.0 270.0 720 76
Example 11
AN 30.0 10.0 1.0 270.0 720 74
__________________________________________________________________________
MMA: Methyl methacrylate, ST: Styrene, AN: Acrylonitrile
As is apparent from Table 5, according to the method of the present invention, a high graft efficiency can be attained with either one of the vinyl monomers (Examples 10 and 11).
The reaction was conducted in the same manner as in Example 1 except that the type of the inorganic compound was changed, and the composition thereby obtained was evaluated. The results are shown in Table 6.
TABLE 6
__________________________________________________________________________
Acid Radical Vinyl Graft
monomer
polymerization
monomer
Deionized
effi-
Inorganic Amount
SEM-Na
BPO MMA water ciency
Compound (parts)
(parts)
(parts) (parts)
(parts)
(%)
__________________________________________________________________________
Example 1
Silicon
270.0
10.0 1.0 30.0 720 92
carbide
Example 2
Zirconium
270.0
10.0 1.0 30.0 720 93
oxide
Example 3
Zirconium
270.0
10.0 1.0 30.0 720 94
nitride
Example 4
Zirconium
270.0
10.0 1.0 30.0 720 91
boride
Example 5
Zirconium
270.0
10.0 1.0 30.0 720 90
carbide
__________________________________________________________________________
As is apparent from Table 6, the method of the present invention is superior to the conventional noncatalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.
As an evaluation of the applicability of the polymeric composition obtained by the method of the present invention to a composite material, a combination of the polymeric composition with polymethyl methacrylate as matrix (inorganic compound content: 80 wt. %) was press-molded at 200° C. under 20 kg/cm2, and the molded product was evaluated for the outer appearance and bending strength. The results are shown in Table 7.
TABLE 7
__________________________________________________________________________
Composite material
composition*.sup.1
Outer
Polymer
Polymeric appearance
Bending
Polymeric content
composition
PMMA of molded
strength
composition (%) (parts)
(parts)
product
(kg/cm.sup.2)
__________________________________________________________________________
Example 13
Example 1 9.6 88 12 ⊚
283
Present invention
Comparative
Compartative Example 1
6.5 86 14 Δ
190
Example 6
Non-catalytic
polymerization
system without
addition of BPO
Comparative
Comparative Example 2
1.1 81 19 X 72
Example 7
No addition of
SEM-Na as opposed
to Example 1
Comparative
Comparative Example 3
4.5 84 16 Δ
140
Example 8
Addition of
dispersant as opposed
to Example 1
Comparative
Non-treated silicon
-- 80 20 64
Example 9
nitride
__________________________________________________________________________
*.sup.1 The ratio of inorganic compound/organic compound = 80/20.
PMMA: Polymethyl methacrylate, Acrypet (VH), manufactured by Mitsubishi
Rayon Co., Ltd.
⊚: Good, Δ: Fair, X: Poor, : Bad
As is apparent from Table 7, according to the method of the present invention (Example 13), a substantial improvement in the effects of the combination is observed with respect to the outer appearance and strength of the molded product.
The polymerization and evaluation were conducted in the same manner as in Example 1 except that methacrylic acid as a carboxylic acid monomer was used instead of the sulfonate monomer. For the purpose of comparison, similar polymerization operation and evaluation after the polymerization were conducted with respect to the polymerization behavior in the cases where no radical polymerization initiator was added as in the conventional non-catalytic polymerization system, no carboxylic acid monomer was added, and a dispersant was added. The results are shown in Table 8.
TABLE 8
__________________________________________________________________________
Carboxylic
Radical Vinyl
Inorganic
Dispersant
acid monomer
polymerization
monomer
compound
Sodium hexa-
Deionized
Conversion
Consolida-
Methyl methacrylic
initiator
MMA Silicon nitride
metaphosphate
water
of monomer
tion rate
acid*.sup.1
BPO (parts)
(parts)
(parts)*.sup.2
(parts) (parts)
(%) (%)*.sup.3
__________________________________________________________________________
Example 14
10.0 1.0 30.0 270.0 -- 720 -100 98
Comparative
10.0 -- 30.0 270.0 -- 720 73 90
Example 10
Comparative
-- 1.0 30.0 270.0 -- 720 90 5
Example 11
Comparative
10.0 1.0 30.0 270.0 3.0 720 93 41
Example 12
__________________________________________________________________________
*.sup.1 CH.sub.2C(CH.sub.3)COOH
*.sup.2 Special grade reagent
##STR6##
BPO: Benzoly peroxide, MMA: Methyl methacrylate
It is evident from Table 8 that in the system where no carboxylic acid monomer was added as in Comparative Example 11, the consolidation rate was very low although the conversion was high, and a tendency for separation of the inorganic compound and the homopolymer was observed. It was further evident that as compared with Comparative Example 10, the method of the present invention is superior in both the conversion of monomer and the consolidation rate. Further, in the system of Comparative Example 12 wherein a dispersant was added, the consolidation rate was substantially low, and a tendency for the separation of the homopolymer was observed as in the case of Comparative Example 11.
The polymeric compositions of Example 14 and Comparative Examples 10 to 12 as shown in Table 8, were continuously extracted by Soxhlet for 50 hours with benzene, 50 hours with acetone and 200 hours with dimethylformamide, as good solvents for methyl methacrylate-methacrylic acid copolymers, whereby the reduction in the polymer contents was studied. The results are shown in Table 9. Here, the polymer content after being thoroughly extracted with dimethylformamide for 200 hours, was evaluated to be a graft rate in the sense that the polymer is firmly consolidated to the surface of the inorganic compound by means of a chemical bond. For the purpose of comparison, a similar extraction operation was conducted with respect to each of compositions (Comparative Examples 13 and 14) wherein an inorganic powder (silicon nitride) was coated, with a polymer obtained by the solvent blending with polymethyl methacrylate or with a methyl methacrylate-methacrylic acid copolymer whereby the reduction in the polymer content was compared.
TABLE 9
__________________________________________________________________________
Polymer content
Graft
Preparation of Polymer content before
continuous extraction*.sup.4
efficiency*.sup.5
2
polymeric composition*.sup.1
extraction (%)
(graft rate)
(%)
__________________________________________________________________________
Polymerization system
Example 14 Presence of methacrylic acid
9.7 9.2 92
(present invention)
Comparative Example 10
Non-catalytic polymerization
6.9 2.0 26
system without addition of BPO
Comparative Example 11
No addition of methacrylic acid
1.1 -0.0 -0
as opposed to Example 14
Comparative Example 12
Addition of dispersant as
4.1 0.7 6.8
opposed to Example 14
Blend system
Comparative Example 13
Solvent blend of polymethyl
9.5 -0.0 --
methacrylate*.sup.2
Comparative Example 14
Solvent blend of methyl methacrylate-
9.6 -0.0 --
methylmethacrylic acid
copolymer*.sup.3
__________________________________________________________________________
*.sup.1 Silicon nitride was used as the inorganic compound.
*.sup.2 Acrypet (VH), manufactured by Mitsubishi Rayon Co., Ltd., was
used.
*.sup.3 A copolymer prepared in the same manner as in Example 14 except
that the method of the present invention was conducted in the absence of
the inorganic compound, was used.
*.sup.4 continuous extraction by Soxhlet for 50 hours with benzene, 50
hours with acetone and 200 hours with dimethylformamide.
##STR7##
The polymer components in the compositions of Comparative Examples 11, 13 and 14 were completely extracted by the above continuous extraction operation irrespective of the system being of a polymerization type or of a solvent blend type. This indicates that even in the polymerization system, a polymer forming in the absence of a carboxylic acid monomer, is merely chemically or physically adsorbed on the surface of the inorganic compound. In Comparative Examples 10 and 12, a part of the formed polymer was firmly consolidated to the inorganic compound, but the level of the graft rate was very low. Whereas, in Example 14 according to the method of the present invention wherein a radical polymerization initiator was added in the presence of a carboxylic acid monomer, the extracted rate after the series of severe extraction operations, was very small, indicating a high graft rate. Further, even when the polymeric composition was subjected to washing treatment with an aqueous NaOH solution, it showed a high graft rate substantially equal to the level after the extraction operations. Thus, it was confirmed that the firm consolidation of the polymer to the surface of the inorganic compound was attributable to the presence of a covalent bond-type graft linkage as a chemical bond stronger than a hydrogen bond or ionic bond at the interface.
The polymerization was carried out in the same manner as in Example 14, except that acrylic acid, crotonic acid, tiglic acid, cinnamic acid or maleic anhydride was used as the carboxylic acid monomer instead of methacrylic acid. The graft efficiency was measured, and the results are shown in Table 10.
TABLE 10
__________________________________________________________________________
Inorganic Graft
Radical polymeri-
Vinyl compound
Deionized
effi-
Carboxylic Amount
zation initiator
monomer
Silicon
water ciency
acid monomer (parts)
BPO (parts)
MMA (parts)
nitride (parts)
(parts)
(%)
__________________________________________________________________________
Example 14
Methacrylic
10.0 1.0 30.0 270.0 720 92
acid
Example 15
Acrylic acid*.sup.1
7.6 1.0 30.0 270.0 720 94
Example 16
Crotonic acid*.sup.2
10.0 1.0 30.0 270.0 720 92
Example 17
Tiglic acid*.sup.3
11.4 1.0 30.0 270.0 720 71
Example 18
Cinnamic acid*.sup.4
16.7 1.0 30.0 270.0 720 78
Example 19
Maleic 11.0 1.0 30.0 270.0 720 90
anhydride*.sup.5
__________________________________________________________________________
*.sup.1 CH.sub.2CHCO.sub.2 H
*.sup.2 CH.sub.3 CHCHCO.sub.2 H
*.sup.3 CH.sub.3 CHC(CH.sub.3)CO.sub.2 H
*.sup.4 C.sub.6 H.sub.5 CHCHCO.sub.2 H
##STR8##
As is apparent from Table 10, the graft efficiency was very high with methacrylic acid, acrylic acid, crotonic acid and maleic anhydride.
The reaction was conducted in the same manner as in Example 14 except that the type of the radical polymerization initiator was changed, and the compositions thereby obtained were evaluated. The results are shown in Table 11.
TABLE 11
__________________________________________________________________________
Radical Carboxylic
Vinyl
Inorganic Graft
polymeri- acid monomer
monomer
compound
Deionized
effi-
zation Amount
Methacrylic
MMA Silicon
water ciency
initiator (parts)
acid (parts)
(Parts)
nitride(parts)
(parts)
(%)
__________________________________________________________________________
Example 14
BPO 1.0 10.0 30.0 270.0 720 92
Example 20
LPO*.sup.1
1.0 10.0 30.0 270.0 720 95
Example 21
AIBN*.sup.2
1.0 10.0 30.0 270.0 720 92
Example 22
AIBA*.sup.3
1.0 10.0 30.0 270.0 720 72
Example 23
KPS*.sup.4
1.0 10.0 30.0 270.0 720 75
__________________________________________________________________________
*.sup.1 Lauroyl peroxide
*.sup.2 Azobisisobutyronitrile
*.sup.3 2,2'-Azobis(2-aminodipropane)hydrochloride
*.sup.4 Potassium persulfate
As is apparent from Table 11, the graft efficiency was higher with lipophilic radical polymerization initiators such as BPO, LPO and AIBN than with water-soluble AIBA and KPS.
The reaction was conducted in the same manner as in Example 14 except that the vinyl monomer identified in Table 12 was used instead of methyl methacrylate as the vinyl monomer, and the compositions thereby obtained were evaluated. The results are shown in Table 12.
TABLE 12
__________________________________________________________________________
Carboxylic Inorganic Graft
acid monomer
Radical compound
Deionized
effi-
Vinyl Amount
Methacrylic
polymerization
Silicon
water ciency
monomer (parts)
acid (parts)
BPO (parts)
nitride(parts)
(parts)
(%)
__________________________________________________________________________
Example 14
MMA 30.0 10.0 1.0 270.0 720 92
Example 24
ST 30.0 10.0 1.0 270.0 720 78
Example 25
AN 30.0 10.0 1.0 270.0 720 72
__________________________________________________________________________
MMA: Methyl methacrylate, ST: Styrene, AN: Acrylonitrile
As is apparent from Table 12, according to the method of the present invention, a high graft efficiency can be attained with either one of the vinyl monomers (Examples 24 and 25). The applicability of a wide range of vinyl monomers is a feature of the present invention in addition to the features of the high conversion and graft rate.
The reaction was conducted in the same manner as in Example 14 except that the type of the inorganic compound was changed, and the composition thereby obtained was evaluated. The results are shown in Table 13.
TABLE 13
__________________________________________________________________________
Carboxylic
Radical poly-
Vinyl Graft
acid monomer
merization
monomer
Deionized
effi-
Inorganic Amount
Methacrylic
BPO MMA water ciency
compound (parts)
acid (parts)
(parts)
(parts)
(parts)
(%)
__________________________________________________________________________
Example 1
Silicon
270.0
10.0 1.0 30.0 720 94
carbide
Example 2
Zirconium
270.0
10.0 1.0 30.0 720 95
oxide
Example 3
Zirconium
270.0
10.0 1.0 30.0 720 96
nitride
Example 4
Zirconium
270.0
10.0 1.0 30.0 720 93
boride
Example 5
Zirconium
270.0
10.0 1.0 30.0 720 92
carbide
__________________________________________________________________________
As is apparent from Table 13, the method of the present invention is superior to the conventional noncatalytic polymerization system in both the polymerization degree and the graft efficiency, and thus indicates that it is capable of providing a polymeric composition of a higher quality.
As an evaluation of the applicability of the polymeric composition obtained by the method of the present invention to a composite material, a combination of the polymeric composition with polymethyl methacrylate as matrix (inorganic compound content: 80 wt. %) was press-molded at 200° C. under 20 kg/cm2, and the molded product was evaluated for the outer appearance and bending strength. The results are shown in Table 14.
TABLE 14
__________________________________________________________________________
Composite material
composition*.sup. 1
Outer
Polymer
Polymeric appearance
Bending
Polymeric content
composition
PMMA of molded
strength
composition (%) (parts)
(parts)
product
(kg/cm.sup.2)
__________________________________________________________________________
Example 27
Example 14 9.7 88 12 ⊚
288
Present invention
Comparative
Comparative Example 10
6.9 86 14 Δ
193
Example 15
Non-catalytic
polymerization
system without
addition of BPO
Comparative
Comparative Example 11
1.1 81 19 X 72
Example 16
No addition of
methacrylic acid as
opposed to Example 14
Comparative
Comparative Example 12
4.1 83 17 Δ
120
Example 17
Addition of
dispersant as opposed
to Example 14
Comparative
Non-treated silicon
-- 80 20 64
Example 18
nitride
__________________________________________________________________________
*.sup.1 The ratio of inorganic compound/organic compound = 80/20.
PMMA: Polymethyl methacrylate, Acrypet (VH), manufactured by Mitsubishi
Rayon Co., Ltd.
⊚: Good, Δ: Fair, X: Poor, : Bad
As is apparent from Table 14, according to the method of the present invention (Example 27), a substantial improvement in the effects of the combination is observed with respect to the outer appearance and strength of the molded product.
Claims (8)
1. A method for preparing a polymeric composition having an inorganic compound firmly consolidated thereinto, which comprises polymerizing at least one radical polymerizable vinyl monomer using a peroxide or azo compound radical initiatior in an aqueous polymerization medium, which medium comprises an inorganic compound dispersed in the presence of an organic acid monomer or organic acid salt monomer, wherein said inorganic compound is selected from the group consisting of a carbide, nitride and boride of silicon and ziroconium, and zirconium oxide; and wherein said organic acid monomer and organic acid salt monomer is a sulfonic acid monomer or sulfonate monomer of the formula: ##STR9## wherein R1 is a hydrogen atom, a C1 -C20 alkyl group or a halogen atom; X is --CONH-- or ##STR10## wherein each of R2 and R3 is a hydrogen atom or a C1 -C15 alkyl group; and R4 is a C1 -C15 alkylene group, --COO(CH2m, wherein m is an integer of 1 to 20 or CH2n, wherein n is an integer of 0 to 20; and Y is a hydrogen atom, an ammonium radical or an alkali metal atom.
2. The method according to claim 1, wherein the inorganic compound is a carbide, nitride or boride of silicon or zirconium.
3. The method according to claim 1, wherein the inorganic compound is zirconium oxide.
4. The method according to claim 1, wherein the sulfonic acid monomer or sulfonate monomer is 2-acrylamido-2-methylpropanesulfonic acid, sodium 2-methacryloylethanesulfonate, sodium 3-methacryloylpropanesulfonate, sodium 2-propenesulfonate or sodium 2-methyl-2-propenesulfonate.
5. The method according to claim 1, wherein the radical polymerization initiator is decomposable at a temperature within a range of from 40° to 100° C.
6. The method according to claim 2, wherein said inorganic compound is silicon carbide.
7. The method according to claim 4, wherein said sulfonate monomer is sodium 2-methacryloylethanesulfonate.
8. The method according to claim 1, wherein said polymerizable vinyl monomer is methyl methacrylate.
Applications Claiming Priority (4)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP18864285A JPS6250313A (en) | 1985-08-29 | 1985-08-29 | Production of polymer composition |
| JP60-188642 | 1985-08-29 | ||
| JP60-188643 | 1985-08-29 | ||
| JP18864385A JPS6250314A (en) | 1985-08-29 | 1985-08-29 | Production of polymer composition |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/246,737 Division US4910251A (en) | 1985-08-29 | 1988-09-20 | Method for preparing a polymeric composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US4783501A true US4783501A (en) | 1988-11-08 |
Family
ID=26505054
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US06/898,496 Expired - Fee Related US4783501A (en) | 1985-08-29 | 1986-08-21 | Method for preparing a polymeric composition |
| US07/246,737 Expired - Fee Related US4910251A (en) | 1985-08-29 | 1988-09-20 | Method for preparing a polymeric composition |
Family Applications After (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US07/246,737 Expired - Fee Related US4910251A (en) | 1985-08-29 | 1988-09-20 | Method for preparing a polymeric composition |
Country Status (3)
| Country | Link |
|---|---|
| US (2) | US4783501A (en) |
| EP (1) | EP0212621B1 (en) |
| DE (1) | DE3689160T2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5210163A (en) * | 1990-06-07 | 1993-05-11 | Arco Chemical Technology, L.P. | Process for preparing alternating copolymers of olefinically unsaturated sulfonate salts and unsaturated dicarboxylic acid anhydrides |
| US5322889A (en) * | 1991-09-24 | 1994-06-21 | Mitsubishi Rayon Co., Ltd. | Composite composition having high transparency and process for producing same |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4762863A (en) * | 1987-03-30 | 1988-08-09 | Mitsubishi Rayon Co., Ltd. | Photopolymerizable dental composition containing a hexafunctional urethane methacrylate based on isocyanuric acid |
| CN112513175B (en) * | 2018-08-03 | 2023-02-21 | 大金工业株式会社 | Fluoropolymer-containing composition and molded article |
Citations (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3265644A (en) * | 1963-02-18 | 1966-08-09 | Nat Lead Co | Particle-polymer compositions and process for making same |
| US3868347A (en) * | 1972-10-17 | 1975-02-25 | Wacker Chemie Gmbh | Process for the production of polyvinyl chloride-coated silicate-containing materials |
| US3884871A (en) * | 1973-06-29 | 1975-05-20 | Nl Industries Inc | Process for coating pigment particles with organic polymers |
| US3904568A (en) * | 1972-02-24 | 1975-09-09 | Lion Fat Oil Co Ltd | Method for grafting organic polymers onto inorganic colloidal material |
| JPS5580412A (en) * | 1978-12-12 | 1980-06-17 | Kanegafuchi Chem Ind Co Ltd | Preparation of vinyl chloride polymer composition |
| US4251576A (en) * | 1974-05-29 | 1981-02-17 | Imperial Chemical Industries Limited | Inorganic reinforcing phase dispersed and bonded to polymer matrix |
| JPS56158140A (en) * | 1980-05-09 | 1981-12-05 | Itaru Yamaguchi | Production of polymer coated body |
| JPS56161461A (en) * | 1980-05-16 | 1981-12-11 | Hitachi Ltd | Resin composition |
| JPS5710604A (en) * | 1980-06-23 | 1982-01-20 | Mitsubishi Rayon Co Ltd | Preparation of novel polymer composition |
| JPS5774301A (en) * | 1980-10-29 | 1982-05-10 | Mitsubishi Rayon Co Ltd | Production of novel polymer composition |
| US4421660A (en) * | 1980-12-15 | 1983-12-20 | The Dow Chemical Company | Colloidal size hydrophobic polymers particulate having discrete particles of an inorganic material dispersed therein |
| US4433097A (en) * | 1980-01-22 | 1984-02-21 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Vinyl chloride resin talc-embedded composition and method of manufacturing same |
| US4435540A (en) * | 1981-01-06 | 1984-03-06 | Mitsubishi Rayon Co., Ltd. | Novel polymer composition |
| US4508761A (en) * | 1982-02-19 | 1985-04-02 | Central Glass Company Limited | Method of preparing polymer-coated particulate inorganic material |
| US4678819A (en) * | 1984-08-30 | 1987-07-07 | Mitsubishi Rayon Co., Ltd. | Compositions for artificial marbles and process for producing artificial marbles therefrom |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3714102A (en) * | 1970-12-02 | 1973-01-30 | Gulf Oil Canada Ltd | Polymer encapsulation of finely divided solids |
| JPS5374118A (en) * | 1976-12-09 | 1978-07-01 | Toa Gosei Chem Ind | Additives for paper making |
| JPS6054630B2 (en) * | 1978-04-21 | 1985-11-30 | 株式会社精工舎 | gear system |
| DE2927249A1 (en) * | 1978-07-07 | 1980-01-17 | Sinloihi Co Ltd | FINE SPHERICAL POLYMER PARTICLES CONTAINING AN INORGANIC PIGMENT AND / OR A BLACK COLORANT, AND METHOD FOR THE PRODUCTION THEREOF |
-
1986
- 1986-08-19 EP EP86111459A patent/EP0212621B1/en not_active Expired - Lifetime
- 1986-08-19 DE DE86111459T patent/DE3689160T2/en not_active Expired - Fee Related
- 1986-08-21 US US06/898,496 patent/US4783501A/en not_active Expired - Fee Related
-
1988
- 1988-09-20 US US07/246,737 patent/US4910251A/en not_active Expired - Fee Related
Patent Citations (16)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3265644A (en) * | 1963-02-18 | 1966-08-09 | Nat Lead Co | Particle-polymer compositions and process for making same |
| US3904568A (en) * | 1972-02-24 | 1975-09-09 | Lion Fat Oil Co Ltd | Method for grafting organic polymers onto inorganic colloidal material |
| US3868347A (en) * | 1972-10-17 | 1975-02-25 | Wacker Chemie Gmbh | Process for the production of polyvinyl chloride-coated silicate-containing materials |
| US3884871A (en) * | 1973-06-29 | 1975-05-20 | Nl Industries Inc | Process for coating pigment particles with organic polymers |
| US4251576A (en) * | 1974-05-29 | 1981-02-17 | Imperial Chemical Industries Limited | Inorganic reinforcing phase dispersed and bonded to polymer matrix |
| JPS5580412A (en) * | 1978-12-12 | 1980-06-17 | Kanegafuchi Chem Ind Co Ltd | Preparation of vinyl chloride polymer composition |
| US4433097A (en) * | 1980-01-22 | 1984-02-21 | Kanegafuchi Kagaku Kogyo Kabushiki Kaisha | Vinyl chloride resin talc-embedded composition and method of manufacturing same |
| JPS56158140A (en) * | 1980-05-09 | 1981-12-05 | Itaru Yamaguchi | Production of polymer coated body |
| JPS56161461A (en) * | 1980-05-16 | 1981-12-11 | Hitachi Ltd | Resin composition |
| JPS5710604A (en) * | 1980-06-23 | 1982-01-20 | Mitsubishi Rayon Co Ltd | Preparation of novel polymer composition |
| JPS5774301A (en) * | 1980-10-29 | 1982-05-10 | Mitsubishi Rayon Co Ltd | Production of novel polymer composition |
| US4421660A (en) * | 1980-12-15 | 1983-12-20 | The Dow Chemical Company | Colloidal size hydrophobic polymers particulate having discrete particles of an inorganic material dispersed therein |
| US4435540A (en) * | 1981-01-06 | 1984-03-06 | Mitsubishi Rayon Co., Ltd. | Novel polymer composition |
| US4546145A (en) * | 1981-01-06 | 1985-10-08 | Mitsubishi Rayon Co., Ltd. | Polymer composition |
| US4508761A (en) * | 1982-02-19 | 1985-04-02 | Central Glass Company Limited | Method of preparing polymer-coated particulate inorganic material |
| US4678819A (en) * | 1984-08-30 | 1987-07-07 | Mitsubishi Rayon Co., Ltd. | Compositions for artificial marbles and process for producing artificial marbles therefrom |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5210163A (en) * | 1990-06-07 | 1993-05-11 | Arco Chemical Technology, L.P. | Process for preparing alternating copolymers of olefinically unsaturated sulfonate salts and unsaturated dicarboxylic acid anhydrides |
| US5322889A (en) * | 1991-09-24 | 1994-06-21 | Mitsubishi Rayon Co., Ltd. | Composite composition having high transparency and process for producing same |
Also Published As
| Publication number | Publication date |
|---|---|
| DE3689160T2 (en) | 1994-05-05 |
| EP0212621A2 (en) | 1987-03-04 |
| US4910251A (en) | 1990-03-20 |
| DE3689160D1 (en) | 1993-11-18 |
| EP0212621B1 (en) | 1993-10-13 |
| EP0212621A3 (en) | 1989-01-25 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| US4546145A (en) | Polymer composition | |
| CA1337163C (en) | Polymeric particles and their preparation | |
| CA1221195A (en) | Use of hydrophobically modified water-soluble polymers in suspension polymerization | |
| US4988771A (en) | Graft copolymer having dispersion stabilizing effect, a process for producing the same, and a process of emulsion polymerization using the same | |
| JP2002537473A5 (en) | ||
| US5916963A (en) | Water-based resin dispersion and process for the production thereof | |
| US4426482A (en) | Process for producing stable polymer emulsions | |
| US4783501A (en) | Method for preparing a polymeric composition | |
| DK0830400T3 (en) | Powders of core / sheath film-forming polymers that are redispersible in water | |
| US3879495A (en) | Impact-resistant rubber-modified plastics and process for producing the same | |
| EP0264721A2 (en) | Thermoplastic resin composition | |
| US5605972A (en) | Graft and core-shell copolymers having improved phase bonding between graft substrate and grafted-on polymer phase | |
| KR100206452B1 (en) | Fluorine-containing graft copolymer and its manufacturing method | |
| JP2648179B2 (en) | Methacrylic resin cast plate excellent in impact resistance and method for producing the same | |
| CS212792B2 (en) | Thermoplastic material and method of manufacturing same | |
| US4853438A (en) | Water-soluble polymers bearing quaternary ammonium or pyridinium groups and alkoxysilyl groups, a method for their preparation, and the use thereof | |
| CA2014022A1 (en) | Precipitation polymerization of copolymers of a vinyl lactam and a polymerizable carboxylic acid in an aliphatic hydrocarbon solvent | |
| EP0528806A1 (en) | Ethylene vinyl silane copolymer and its preparation | |
| JPH0549704B2 (en) | ||
| JPH01299810A (en) | Graft copolymer, polymer material composition containing said copolymer and foamable polystyrene bead containing said copolymer and preparation of said bead | |
| JPS6250314A (en) | Production of polymer composition | |
| JPS62288618A (en) | Transparent resin | |
| JPS61118130A (en) | Aqueous dispersion stabilizer of fine-particle silica powder | |
| JP2505842B2 (en) | Electrorheological fluid composition | |
| AU2003276535A1 (en) | Copolymers comprising unsaturation and process for preparation thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: MITSUBISHI RAYON CO., LTD., 3-19, KYOBASHI 2-CHOME Free format text: ASSIGNMENT OF ASSIGNORS INTEREST.;ASSIGNORS:SASAKI, ISAO;MUKAI, NOBUHIRO;IGE, HITOSHI;REEL/FRAME:004928/0447 Effective date: 19860812 Owner name: MITSUBISHI RAYON CO., LTD., JAPAN Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:SASAKI, ISAO;MUKAI, NOBUHIRO;IGE, HITOSHI;REEL/FRAME:004928/0447 Effective date: 19860812 |
|
| FEPP | Fee payment procedure |
Free format text: PAYOR NUMBER ASSIGNED (ORIGINAL EVENT CODE: ASPN); ENTITY STATUS OF PATENT OWNER: LARGE ENTITY |
|
| FPAY | Fee payment |
Year of fee payment: 4 |
|
| FPAY | Fee payment |
Year of fee payment: 8 |
|
| REMI | Maintenance fee reminder mailed | ||
| LAPS | Lapse for failure to pay maintenance fees | ||
| FP | Lapsed due to failure to pay maintenance fee |
Effective date: 20001108 |
|
| STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |